chemical engineering vol 2 particle technology and separation processes 5ed
chemical engineering vol 2 particle technology and separation processes 5ed
... µmin.µmin.µmin.µm 325 0.0017 43 325 0.0017 44 27 0 0.0 021 53 27 0 0.0 021 53 300 0.0 021 53 25 0 0.0 024 61 23 0 0.0 024 61 24 0 0.0 026 66 20 0 0.0 025 63 20 0 0.0 029 74 20 0 0.0 029 74 20 0 0.0030 76 170 0.0034 ... 0.0 125 347 42 0.0133 351 35 0.0197 500 44 0.0139 353 35 0.0164 417 30 0. 023 2 590 36 0.0166 422 30 0.0166 422 32 0.0195 495 30 0.0197 500 28 0. 023 2 589 25 0....
Ngày tải lên: 04/06/2014, 13:14
coulson and richardson - chemical engineering vol. 2 particle technology and separation processes (5th ed)
... 14.18, 14.19, 14 .20 . APV Baker Ltd, Crawley, Sussex for Figs. 14 .21 , 14 .22 , 14 .23 , 14 .24 , 14 .25 , 14 .26 . The Editor and Publishers of Chemical and Process Engineering for Figs. 14 .28 , 14.30. APV ... Figs. 2. 4, 2. 7, 2. 13, 2. 14, 2. 29. Hadfields Ltd for Fig. 2. 5. Hosokawa Micron Ltd, Runcorn, Cheshire for Fig. 2. 12. Babcock & Wilcox Ltd for Fig. 2. 19. P...
Ngày tải lên: 01/04/2014, 11:16
coulson & richardson - solutions to the problems in chemical engineering volume 2 & 3
... nd 2 nd 3 1 20 00 20 00 20 00 3 600 5400 16 ,20 0 6 140 5040 30 ,24 0 10 40 4000 40,000 14 15 29 40 41,160 18 5 1 620 29 ,160 22 2 968 21 ,29 6 = 21 ,968 = 180,056 Thus: d s = (180,056 /21 ,968) = 8 .20 ... mN s/m 2 1 day 86.4 ks 1 stoke 10 −4 m 2 /s 1year 31.5Ms 1ft 2 /h 0 .25 8 cm 2 /s area mass flow 1in 2 645 .2 mm 2 1 lb/h 0. 126 g/s 1ft 2 0.093 m 2 1 ton/h...
Ngày tải lên: 01/04/2014, 11:15
coulson & richardson_s chemical engineering. vol. 6 chemical engineering design 4th ed
... Mixtures 322 8.9 Specific heat capacity 322 8.9.1 Solids and liquids 322 8.9 .2 Gases 325 8.10 Enthalpy of vaporisation (latent heat) 328 8.10.1 Mixtures 329 8.11 Vapour pressure 330 8. 12 Diffusion ... kettle reboilers 750 12. 12 Plate heat exchangers 756 12. 12. 1 Gasketed plate heat exchangers 756 12. 12. 2 Welded plate 764 12. 12. 3 Plate-fin 764 12. 12. 4 Spiral heat exchan...
Ngày tải lên: 01/04/2014, 11:15
handbook of reactive chemical hazards vol 2 (bretherick 1999)
... 1 521 4-Ethoxy -2- methyl-3-butyn -2- ol, 28 44 1-Ethoxy -2- propyne, 1909 2- Ethynylfuran, 22 12 Ethynyl vinyl selenide, 1449 2- Heptyn-1-ol, 28 41 4,5-Hexadien -2- yn-1-ol, 23 28 2, 4-Hexadiyne-1,6-dioic acid, 20 94 2, 5-Hexadiyn-1-ol, 23 29 1,5-Hexadiyn-3-one, ... 20 94 2, 5-Hexadiyn-1-ol, 23 29 1,5-Hexadiyn-3-one, 22 13 2, 4-Hexadiynylene chloroformate, 28 90 2, 4-Hexad...
Ngày tải lên: 09/05/2014, 17:01
chemical engineering vol 5 coulson & richardson's
... nd 2 nd 3 1 20 00 20 00 20 00 3 600 5400 16 ,20 0 6 140 5040 30 ,24 0 10 40 4000 40,000 14 15 29 40 41,160 18 5 1 620 29 ,160 22 2 968 21 ,29 6 = 21 ,968 = 180,056 Thus: d s = (180,056 /21 ,968) = 8 .20 ... mN s/m 2 1 day 86.4 ks 1 stoke 10 −4 m 2 /s 1year 31.5Ms 1ft 2 /h 0 .25 8 cm 2 /s area mass flow 1in 2 645 .2 mm 2 1 lb/h 0. 126 g/s 1ft 2 0.093 m 2 1 ton/h...
Ngày tải lên: 04/06/2014, 13:18
chemistry and chemical engineering research progress (chemical engineering methods and technology)
... stabilized ZrO 2 -TiN (60/40 vol% ), 2 mol% yttria stabilized ZrO 2 -WC (60/40 vol% ) and 2 mol% yttria stabilized ZrO 2 -NbC with 40 or 50 vol% NbC. Details on the starting powders and powder preparation ... of 0 .2- 0.3 MPa (2- 3 bar) up to 125 0°C. In step 2, the pressure is decreased to 2 × 10 -3 MPa (2E -2 bar) at 125 0°C and the samples are heated further at...
Ngày tải lên: 01/04/2014, 10:12